EP3253233B1 - Microcapsules comprenant de la lutéine ou ester de lutéine - Google Patents

Microcapsules comprenant de la lutéine ou ester de lutéine Download PDF

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Publication number
EP3253233B1
EP3253233B1 EP16703761.3A EP16703761A EP3253233B1 EP 3253233 B1 EP3253233 B1 EP 3253233B1 EP 16703761 A EP16703761 A EP 16703761A EP 3253233 B1 EP3253233 B1 EP 3253233B1
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Prior art keywords
lutein
microcapsule
bloom
fish gelatine
microcapsules
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German (de)
English (en)
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EP3253233A1 (fr
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Nina Musaeus
Inge-Lise KRYLBO
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BASF SE
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BASF SE
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    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09B—ORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B67/00—Influencing the physical, e.g. the dyeing or printing properties of dyestuffs without chemical reactions, e.g. by treating with solvents grinding or grinding assistants, coating of pigments or dyes; Process features in the making of dyestuff preparations; Dyestuff preparations of a special physical nature, e.g. tablets, films
    • C09B67/0097—Dye preparations of special physical nature; Tablets, films, extrusion, microcapsules, sheets, pads, bags with dyes
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/30—Encapsulation of particles, e.g. foodstuff additives
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52—Adding ingredients
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52—Adding ingredients
    • A23L2/58—Colouring agents
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L29/00—Foods or foodstuffs containing additives; Preparation or treatment thereof
    • A23L29/20—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents
    • A23L29/275—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents of animal origin, e.g. chitin
    • A23L29/281—Proteins, e.g. gelatin or collagen
    • A23L29/284—Gelatin; Collagen
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/105—Plant extracts, their artificial duplicates or their derivatives
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/115—Fatty acids or derivatives thereof; Fats or oils
    • A23L33/12—Fatty acids or derivatives thereof
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/15—Vitamins
    • A23L33/155—Vitamins A or D
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L5/00—Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
    • A23L5/40—Colouring or decolouring of foods
    • A23L5/42—Addition of dyes or pigments, e.g. in combination with optical brighteners
    • A23L5/43—Addition of dyes or pigments, e.g. in combination with optical brighteners using naturally occurring organic dyes or pigments, their artificial duplicates or their derivatives
    • A23L5/44—Addition of dyes or pigments, e.g. in combination with optical brighteners using naturally occurring organic dyes or pigments, their artificial duplicates or their derivatives using carotenoids or xanthophylls
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00—Medicinal preparations containing organic active ingredients
    • A61K31/01—Hydrocarbons
    • A61K31/015—Hydrocarbons carbocyclic
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00—Medicinal preparations containing organic active ingredients
    • A61K31/045—Hydroxy compounds, e.g. alcohols; Salts thereof, e.g. alcoholates
    • A61K31/047—Hydroxy compounds, e.g. alcohols; Salts thereof, e.g. alcoholates having two or more hydroxy groups, e.g. sorbitol
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00—Medicinal preparations containing organic active ingredients
    • A61K31/045—Hydroxy compounds, e.g. alcohols; Salts thereof, e.g. alcoholates
    • A61K31/07—Retinol compounds, e.g. vitamin A
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00—Medicinal preparations containing organic active ingredients
    • A61K31/21—Esters, e.g. nitroglycerine, selenocyanates
    • A61K31/215—Esters, e.g. nitroglycerine, selenocyanates of carboxylic acids
    • A61K31/22—Esters, e.g. nitroglycerine, selenocyanates of carboxylic acids of acyclic acids, e.g. pravastatin
    • A61K31/23—Esters, e.g. nitroglycerine, selenocyanates of carboxylic acids of acyclic acids, e.g. pravastatin of acids having a carboxyl group bound to a chain of seven or more carbon atoms
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/141—Intimate drug-carrier mixtures characterised by the carrier, e.g. ordered mixtures, adsorbates, solid solutions, eutectica, co-dried, co-solubilised, co-kneaded, co-milled, co-ground products, co-precipitates, co-evaporates, co-extrudates, co-melts; Drug nanoparticles with adsorbed surface modifiers
    • A61K9/146—Intimate drug-carrier mixtures characterised by the carrier, e.g. ordered mixtures, adsorbates, solid solutions, eutectica, co-dried, co-solubilised, co-kneaded, co-milled, co-ground products, co-precipitates, co-evaporates, co-extrudates, co-melts; Drug nanoparticles with adsorbed surface modifiers with organic macromolecular compounds
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/14—Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16—Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • A61K9/167—Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction with an outer layer or coating comprising drug; with chemically bound drugs or non-active substances on their surface
    • A61K9/1676—Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction with an outer layer or coating comprising drug; with chemically bound drugs or non-active substances on their surface having a drug-free core with discrete complete coating layer containing drug
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/48—Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/5005—Wall or coating material
    • A61K9/5021—Organic macromolecular compounds
    • A61K9/5052—Proteins, e.g. albumin
    • A61K9/5057—Gelatin
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/48—Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/5005—Wall or coating material
    • A61K9/5063—Compounds of unknown constitution, e.g. material from plants or animals
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/48—Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/51—Nanocapsules; Nanoparticles
    • A61K9/5107—Excipients; Inactive ingredients
    • A61K9/5123—Organic compounds, e.g. fats, sugars
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00—Medicinal preparations characterised by special physical form
    • A61K9/48—Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50—Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • A61K9/51—Nanocapsules; Nanoparticles
    • A61K9/5107—Excipients; Inactive ingredients
    • A61K9/513—Organic macromolecular compounds; Dendrimers
    • A61K9/5169—Proteins, e.g. albumin, gelatin
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P3/00—Drugs for disorders of the metabolism
    • A61P3/02—Nutrients, e.g. vitamins, minerals
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09B—ORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
    • C09B61/00—Dyes of natural origin prepared from natural sources, e.g. vegetable sources
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2250/00—Food ingredients
    • A23V2250/54—Proteins
    • A23V2250/542—Animal Protein
    • A23V2250/5432—Gelatine

Definitions

  • the present invention relates to a microcapsule comprising lutein or lutein esters as active substance embedded in a hydrocolloid matrix of low bloom fish gelatine, a process for preparing such microcapsules as well as applications thereof and products comprising such microcapsules.
  • Lutein is a xanthophyll and a naturally occurring carotenoid found in plants, such as flowers, in particular marigold flowers, and green leafy vegetables. Lutein may for instances be extracted from the petals of marigold, spinach, kale and broccoli. Marigold is in particular rich in lutein, and it is found as lutein esters with fatty acids. Lutein can be used as yellow pigment in all kind of compositions, such as functional foods and health care products, and it has well known pharmacological effects and applications.
  • Lutein as free lutein has the chemical structure
  • the typical lutein esters found in marigold are the mono- or dipalmitate, and these esters have properties different from the free lutein.
  • the molecular weight of free lutein is about 569 g/mol, whereas the molecular weight of the dipalmitate is about 1046 g/mol.
  • the melting point of free lutein is about 190 °C, whereas the melting range of the mixed naturally occurring lutein esters is from about 50 to about 80 °C.
  • Chinese patent application 102389108 A discloses lutein ester microcapsule powder comprising lutein ester crystals, antioxidants and emulsifying agents for both the oil-phase and the aqueous-phase, filler, wall material and oil, and a method for preparing the same.
  • the filler material applied is modified gum arabic or modified starch.
  • emulsifiers in the formulation has the disadvantages that air will be trapped into the powder particles and form hollow spheres. The included air and the porosity of the microcapsules lead to chemical degradation of the lutein or lutein ester.
  • Using emulsifiers furthermore has the disadvantage that the preparation is more expensive and time consuming to produce because the emulsifiers have to be mixed thoroughly with the other ingredients in the aqueous and the oil phase, respectively. Furthermore the list of ingredients in the powder formulation increases.
  • EP 1 794 238 B1 discloses a carotenoid-containing dry powder comprising one or more carotenoids such as crystalline lutein obtainable by a microencapsulation process using isomalt and a protective colloid such as modified starch as encapsulation material, wherein the initial suspension of crystalline carotenoids is grounded.
  • EP 1 898 721 B1 discloses an aqueous carotenoid-containing suspension comprising at least one or more carotenoids such as crystalline lutein, modified starch and sucrose, wherein the initial suspension of crystalline carotenoids is grounded.
  • WO2014/154788 discloses a powderous composition comprising particles of lutein and maltodextrin as matrix material.
  • US 2003/148099 discloses microcapsules having a carotenoid content of from 10 to 50 % by weight and a protective coating, such as a coating of high bloom fish gelatin having a bloom strength of 180-220.
  • EP 1 105 099 discloses a particulate composition comprising an active substance and a protective colloid of fish gelatine having a bloom strength of above 100 bloom, preferably above 200 bloom.
  • EP 1 938 807 discloses microcapsules comprising an active substance, such as lutein, in an unspecified gelatine matrix also comprising a powdering agent.
  • US 5 780 056 discloses a microcapsule of multi-core structure comprising carotenoid particles embedded in a matrix comprising gelatine of at least 100.
  • US 2206/165990 discloses a microcapsule comprising an agglomeration of primary microcapsules and a loading substance; the microcapsule comprises a primary shell and outer shell.
  • the main object of the present invention is to provide improved products based on lutein or lutein ester concentrates and fish gelatine which shall have a cleaner label and fewer ingredients. They shall have or create in the final product a more intense and longer lasting colour impression and they shall be more stable and less sensitive to oxidation compared with state of the art products. They shall exhibit a surface, said surface being more adapted for compression than surfaces of products of the prior art. They shall exhibit a greater chemical stability and be more natural in composition. They shall be produced in an easier and more cost effective way.
  • Another object is to provide improved products based on lutein or lutein ester concentrates and fish gelatine which can be used in tablets, dairies, such as milk products, and beverages with high stability due to proper encapsulation of the lutein and/or lutein ester and with improved oxygen barrier properties.
  • Yet another object is to provide a cost effective method for producing such products.
  • the present invention relates to a microcapsule comprising at least one active substance selected from lutein and lutein esters, embedded in a matrix comprising low bloom fish gelatine having a strength of 100 bloom or less and optionally one or more other matrix components, wherein the content of said at least one active substance calculated as free lutein is from 0.5 to 25 % of total weight of the microcapsule, and which microcapsule does not comprise any added emulsifier.
  • the microcapsule does not comprise any added oil phase emulsifier.
  • the microcapsule of the invention can be provided without any added dispersing agent or emulsifier in addition to the fish gelatine. Accordingly, the fish gelatine is the sole agent with dispersing properties present in the microcapsule.
  • a classical emulsifier is included in a microcapsule to ensure a sufficiently small particle size, and a small particle size is important for the appearance and colour of the final product comprising the microcapsules, such as dairies and beverages.
  • the absence of any added classical emulsifier has also the advantage in comparison with prior art microcapsules comprising lutein and lutein esters that foaming during preparation is avoided. Foaming during preparation will lead to inclusion of air in the microcapsules which will decrease the chemical stability of the lutein or lutein ester in the final product.
  • a product without any added emulsifier provides the advantage of a cleaner label.
  • the present invention in another aspect relates to a process of preparing a microcapsule according to the invention, which process comprises the steps of
  • the invention relates to the microcapsule according to the invention obtainable according to the process of the invention.
  • the invention relates to products comprising the microcapsule of the invention, in particular dairies, beverages and tablets.
  • Lutein ester concentrate is a dark orange-brown oleoresin or a granular powder having a melting range of approximately 50-80 °C. It typically comprises 70-85 % lutein ester, corresponding to about half the amount of free lutein. It can be dissolved or melted in oil.
  • Lutein ester concentrate complies with the EFSA (European Food Safety Authority) specification for lutein (Directive 2008/128/EC (E 161b)).
  • the main colouring principle of lutein consists of carotenoids of which lutein and its fatty esters account for the major part.
  • Variable amounts of other carotenes and xanthophyll esters, such as zeaxanthin ester, are also present in the concentrate.
  • Lutein may contain fats, oils and waxes naturally occurring in the plant material.
  • Lutein ester concentrate contains min. 60% total carotenoid esters.
  • Fish gelatine is in this context defined as a protective hydrocolloid with dispersing properties.
  • it is not to be understood as a classical emulsifier (surfactant) in accordance with the definition below.
  • Low bloom, medium bloom and high bloom fish gelatines are gelatins having a strength of less than about 120 bloom (low bloom), between 120 and 200 bloom (medium bloom) or a strength of more than about 200 bloom (high bloom.)
  • Low bloom fish gelatine in particular means a fish gelatine having a strength of 100 bloom or less, more preferably 80 bloom or less, more preferably from zero to 80 bloom, still more preferred from zero bloom to 50 bloom.
  • low bloom fish gelatine means a fish gelatine having a strength of about 50 bloom or less, preferably of about 30 bloom or less, more preferably of about 20 bloom or less and further preferred of about 10 bloom or less.
  • a particular preferred embodiment of low bloom fish gelatine comprises a fish gelatine having a strength of zero bloom.
  • An emulsifier is defined as a substance with a hydrophilic head and a hydrophobic tail. Emulsifiers can be divided into non-ionic, anionic and cationic emulsifiers. Depending on the HLB-value (hydrophilic-lipophilic balance) emulsifiers can be either oil soluble (low HLB values) or water soluble (high HLB values). Adding both types to an emulsion often works synergistic. Typical emulsifiers allowed in food products comprise glycerol fatty acid esters, sucrose fatty acid esters, sorbitan fatty acid esters, lecithins, ascorbyl palmitate and ascorbyl stearate.
  • Dispersing means mixing one phase (the continuous phase) with a second phase (the disperse phase) where the two phases not being miscible to prepare a dispersion.
  • the nature of each phase can be liquid, solid or gaseous.
  • Homogenising means treating a dispersion in order to reduce the size of the droplets/particles of the disperse phase.
  • Bloom is a test to measure the strength of a gel of gelatine. The test determines the weight (in grams) needed by a probe (normally with a diameter of 0.5 inch) to deflect the surface of the gel 4 mm without breaking it. The result is expressed in bloom (grades).
  • Morphology means the shape and structure of a physical object, in the context of this invention the shape and structure of a microcapsule.
  • the color strength (E 0.1% 1cm -value) is here defined as the absorption of a 1% aqueous dispersion of a 10 % lutein or lutein ester dry powder measured in a 1 cm cuvette at the wavelength of the absorption maximum.
  • Tablet stability means the chemical stability of lutein or lutein ester added as a microencapsulated powder to multivitamin mineral tablets stored under controlled conditions and followed over time.
  • Fig. 1 and Fig. 2 The appearance and surface morphology of the microcapsules of the invention in comparison with FloraGLO® Lutein 10% VG TabGrade microcapsules from Kemin Health, L.C. are illustrated in Fig. 1 and Fig. 2 , wherein:
  • the content of said at least one active substance, calculated as free lutein is from 1 to 20 % of total weight of the microcapsule, preferably from 3 to 15 % more preferably from 4 to 13 %, for instance from 5 to 10 % of total weight of the microcapsule.
  • the microcapsule of the invention comprises at least one antioxidant e.g. selected from the group essentially consisting of or comprising t-butylhydroxytoluene (BHT), t-butylhydroxyanisole (BHA), ascorbic acid, sodium ascorbate, citric acid, sodium citrate, EDTA or its salts, tocopherols, TBHQ, ethoxyquine, propyl gallate, and extracts from herbs, i.a. rosemary or oregano extract.
  • BHT t-butylhydroxytoluene
  • BHA t-butylhydroxyanisole
  • the microcapsule comprises at least one plasticizer, e.g. selected from the group essentially consisting of or comprising carbohydrates and carbohydrate alcohols, examples of which are sucrose, glucose, fructose, lactose, invert sugar, glucose syrup, sorbitol, mannitol, trehalose, tagatose, pullulan, Raftilose (oligofructose), dextrin, maltodextrin, glycerin and mixtures thereof.
  • plasticizer e.g. selected from the group essentially consisting of or comprising carbohydrates and carbohydrate alcohols, examples of which are sucrose, glucose, fructose, lactose, invert sugar, glucose syrup, sorbitol, mannitol, trehalose, tagatose, pullulan, Raftilose (oligofructose), dextrin, maltodextrin, glycerin and mixtures thereof.
  • the microcapsule comprises low bloom fish gelatine having a strength of 30 bloom or less preferably of 20 bloom or less and more preferably of 10 bloom or less.
  • the microcapsule comprises lutein ester(s) as active substance.
  • this microcapsule has the further advantage that the lutein ester(s) is the naturally occurring form of the lutein. Producing free lutein from a marigold extract requires saponification under harsh conditions. This processing step is avoided when using lutein ester(s) in the microcapsule.
  • the mircrocapsule is prepared form an emulsion of melted or dissolved lutein or lutein ester concentrate(s) in an aqeouos solution of the fish gelatine in the absence of an emulsifier, wherein said lutein or lutein ester concentrate(s) is optionally melted or dissolved in an edible oil.
  • the lutein/lutein ester droplets have an average size D[4;3] determined by Fraunhofer diffraction of from 0.02 to 100 ⁇ m, preferably 0.05 to 50 ⁇ m, more preferred 0.1 to 5 ⁇ m or 0.2 to 1.5 ⁇ m; and in particular from 0.1 to 0.5 ⁇ m.
  • D[4;3] is explained in the introduction to the examples.
  • the microcapsule is prepared from non-crystalline lutein ester.
  • the microcapsule may further contain conventional additives e.g. selected from the group essentially consisting of or comprising anti-caking agents, e.g. tri-calcium phosphate and silicates, i.a. silicon dioxide and sodium aluminium silicate.
  • anti-caking agents e.g. tri-calcium phosphate and silicates, i.a. silicon dioxide and sodium aluminium silicate.
  • the dividing and drying of the mixture of the oil-in-water preparation to produce a mass of particles can be done in any conventional way, such as spray cooling, modified spray cooling, spray drying, modified spray drying or sheet drying and crushing, see e.g. WO 91/06292 A1 .
  • the lutein or lutein ester concentrate(s) is melted or dissolved in edible oil, such as vegetable oil, e.g. selected from the group essentially consisting of or comprising sunflower oil, olive oil, cotton seed oil, safflower oil, MCT oil, palm oil or hydrogenated palm oil. Melting or dissolving the lutein or lutein ester in an oil facilitates dispersing and homogenising and reduces the temperature to be applied.
  • edible oil such as vegetable oil, e.g. selected from the group essentially consisting of or comprising sunflower oil, olive oil, cotton seed oil, safflower oil, MCT oil, palm oil or hydrogenated palm oil.
  • the process of the invention may in a second embodiment comprise a further step of homogenisation, such as high pressure homogenisation.
  • the aqueous solution of fish gelatine preferably low bloom fish gelatine
  • the aqueous solution of fish gelatine is added to the melted or dissolved lutein or lutein ester concentrate(s) before homogenisation. Adding the aqueous phase to the oil phase minimizes physical loss of the lutein or lutein ester.
  • the melted or dissolved lutein or lutein ester concentrate(s) is added to the aqueous solution of fish gelatine, preferably low bloom fish gelatine, before homogenisation.
  • the lutein or lutein ester concentrate(s) is added to the aqueous solution of fish gelatine, preferably low bloom fish gelatine, and melted during heating before homogenisation. This is preferred if the lutein or lutein ester is not melted or dissolved in oil before homogenisation because it is a more simple process and the physical loss is minimized.
  • the homogenisation continues until the lutein/lutein ester droplets have an average size D[4;3] determined by Fraunhofer diffraction of from 0.02 to 100 ⁇ m, preferably 0.05 to 50 ⁇ m, more preferred 0.1 to 5 ⁇ m or 0.2 to 1.5 ⁇ m; and in particular from 0.1 to 0.5 ⁇ m.
  • D[4;3] is explained in the introduction to the examples.
  • Lutein ester concentrate(s) is melted or dissolved.
  • Lutein ester has a lower melting point than free lutein, and this makes it possible, in this embodiment of the invention, to melt or dissolve the lutein ester under atmospheric pressure and to use it directly in the process. This process includes less harsh conditions, and is therefore more cost effective than the process which uses free lutein.
  • the present invention also relates to a product comprising microcapsules of the invention or microcapsules produced according to the invention.
  • a product comprising microcapsules of the invention or microcapsules produced according to the invention.
  • examples of such products are a tablet, a beverage, a dairy, a food, a food supplement, a pharmaceutical or veterinary product, a feed or feed supplement, a personal care product or a household product.
  • the content of lutein ester and free lutein in the microcapsules is determined as follows:
  • the lutein or lutein ester is released from the microcapsules under mild alkaline conditions using alkalase and heat.
  • the lutein or lutein ester is extracted by means of ethanol and diethyl ether in a ratio of 2:5 and an aliquot of this extraction is dissolved in a known volume of ethanol.
  • Homogenisation is performed in conventional homogenisation equipment. Homogenisation takes place until the oil droplets have the intended average size D[4;3] determined by Fraunhofer diffraction.
  • D[4;3] refers to the volume-weighted average diameter (see Operators Guide, Malvern Mastersizer 2000, Malvern Instruments Ltd., 1998/1999, UK, Chapter 6, page 6.3 ).
  • Multivitamin mineral tablets with a content of approximately 2 mg lutein ester (or 1 mg lutein) per tablet were prepared.
  • the tablets were filled in HDPE containers sealed with an alumina lid. Some containers were stored at 40°C/75% RH for 6 months, some containers were stored at 25°C/60% RH for 12 months.
  • the content of lutein/lutein ester in the tablets was analyzed after 3 and 6 months for the tablets stored at 40°C/75% RH and after 6 and 12 months for the tablets stored at 25°C/60% RH . The remaining lutein/lutein ester of the initial value was calculated in each timepoint.
  • vessel A 400 g dry low bloom, preferable zero bloom, fish gelatine, 400 g sucrose and 25 g sodium ascorbate were dissolved in 600 g water at 65°C during stirring.
  • vessel B 250 g lutein ester concentrate was melted together with 62.5 g sunflower oil and 17.9 g mixed tocopherols (70% concentrate) at 60-90°C.
  • the oily phase from vessel B was added to the aqueous phase in vessel A during stirring followed by homogenisation until the lutein ester droplets had an average particle size D[4;3] of less than 1.0 ⁇ m.
  • the viscosity was adjusted with water and the dispersion was sprayed into native corn starch containing silicon dioxide as a flow agent. The formed particles were dried in air at 40-150°C until the water content in the powder was below 5%.
  • the resulting dried powder had a content of 11.9% lutein esters corresponding to 6.4 % free lutein determined by UV/Vis spectroscopy.
  • the color strength (E 01% 1cm ) of the product was 91.
  • vessel A 400 g dry low bloom, preferable zero bloom, fish gelatine, 400 g sucrose and 25 g sodium ascorbate were dissolved in 600 g water at 65°C during stirring.
  • vessel B 250 g lutein ester concentrate was melted together with 62.5 g sunflower oil and 17.9 g mixed tocopherols (70% concentrate) at 60-90°C.
  • the oily phase from vessel B was added to the aqueous phase in vessel A during stirring followed by homogenisation until the lutein ester droplets had an average particle size D[4;3] of less than 1.0 ⁇ m.
  • the viscosity was adjusted with water and the dispersion was sprayed into native corn starch containing silicon dioxide as a flow agent. The formed particles were dried in air at 40-150°C until the water content in the powder was below 5%.
  • the resulting dried powder had a content of 12.4% lutein esters corresponding to 6.68 % free lutein determined by UV/Vis spectroscopy.
  • the color strength (E 0.1% 1cm ) of the product was 78.
  • 400 g dry low bloom, preferable zero bloom, fish gelatine, 400 g sucrose and 25 g sodium ascorbate were dissolved in 600 g water at 65°C during stirring.
  • 250 g lutein ester concentrate, 62.5 g sunflower oil and 17.9 g mixed tocopherols (70% concentrate) were added during stirring followed by homogenisation until the lutein ester droplets had an average particle size D[4;3] of less than 1.0 ⁇ m.
  • the viscosity was adjusted with water and the dispersion was sprayed into native corn starch containing silicon dioxide as a flow agent. The formed particles were dried in air at 40-150°C until the water content in the powder was below 5%.
  • the resulting dried powder had a content of 13.5% lutein esters corresponding to 7.27 % free lutein determined by UV/Vis spectroscopy.
  • the color strength (E 0.1% 1cm ) of the product was 86.
  • vessel A 1060 g dry low bloom, preferable zero bloom, fish gelatine, 1060 g sucrose and 62.5 g sodium ascorbate were dissolved in 1500 g water at 65°C during stirring.
  • vessel B 625 g lutein ester concentrate was melted together with 62.5 g sunflower oil and 44.6 g d,l- ⁇ -tocopherol at 60-90°C.
  • the aqueous phase from vessel A was added to the oil phase in vessel B during stirring followed by homogenisation until the lutein ester droplets had an average particle size D[4;3] of less than 1.0 ⁇ m.
  • the viscosity was adjusted with water and the dispersion was sprayed into native corn starch containing silicon dioxide as a flow agent. The formed particles were dried in air at 40-150°C until the water content in the powder was below 5%.
  • the resulting dried powder had a content of 11.1% lutein esters corresponding to 5.98 % free lutein determined by UV/Vis spectroscopy.
  • the color strength (E 0.1% 1cm ) of the product was 91.
  • vessel A 1251 g dry low bloom, preferable zero bloom, fish gelatine, 1251 g sucrose and 62.5 g sodium ascorbate were dissolved in 2063 g water at 65°C during stirring.
  • vessel B 625 g lutein ester concentrate was melted together with 62.5 g sunflower oil and 44.6 g mixed tocopherols (70% concentrate) at 60-90°C.
  • the aqueous phase from vessel A was added to the oil phase in vessel B during stirring followed by homogenisation until the lutein ester droplets had an average particle size D[4;3] of less than 1.0 ⁇ m.
  • the viscosity was adjusted with water and the dispersion was sprayed into native corn starch containing tricalcium phosphate as a flow agent. The formed particles were dried in air at 40-150°C until the water content in the powder was below 5%.
  • the resulting dried powder had a content of 10.8 % lutein esters corresponding to 5.82 % free lutein determined by UV/Vis spectroscopy.
  • the color strength (E 01% 1cm ) of the product was 81.
  • microcapsules prepared according to the examples were tested for stability in milk and beverages and the chemical stability of the lutein ester was tested in multivitamin mineral tablets as shown in the preamble to the examples and infra after the comparative example.
  • Fig. 1 shows scanning electron micrograph (SEM) pictures of the surface of microcapsules according to the invention (left) and of FloraGLO Lutein 10% VG TabGrade microcapsules (right). It can be clearly seen that the surface morphology of the microcapsules is different for the two types of microcapsules.
  • a thin layer of insoluble starch covers the microcapsules of the invention and they have a rough structure compared to FloraGLO Lutein 10% VG TabGrade microcapsules, which are more smooth.
  • Such rough structured microcapsules of the invention are more adapted for compression into tablets, since their compressibility is larger compared to smooth FloraGLO Lutein 10% VG TabGrade microcapsules.
  • Fig. 2 shows the UV/Vis-absorption spectra of redispersed microcapsules in a concentration of 5 ppm lutein or lutein ester.
  • the upper black curve is the absorption spectrum of the redispersed microcapsules of example 4 of the invention
  • the lower grey curve is the absorption spectrum of redispersed FloraGLO 10% VG microcapsules from Kemin Health L.C..
  • the color strength of the redispersed micorcapsules can be calculated by multiplying the absorption at maximum wavelength with 200 . It can be seen that the absorption is much higher for the microcapsules of the invention compared to FloraGLO® Lutein 10 % VG TabGrade microcapsules. This means, that the color strength of redispersed microcapsules of the invention is much higher than that of the comparative redispersed product from Kemin Health L.C.
  • the chemical stability of the lutein ester microcapsules was tested by means of multivitamin mineral tablets having a content of about 2 mg of lutein ester per tablet.
  • the tablets were packaged in high density polyethylene (HDPE) containers whose lids were sealed with heat-sealed aluminum foil.
  • HDPE high density polyethylene
  • Fig.3 graphically shows the chemical stability in multivitamin mineral tablets, as indicated in tables 1A and 1B, of microcapsules according to examples 2 and 4 of the invention and compared to multivitamin tablets of FloraGLO Lutein 10% VG TabGrade microcapsules.
  • the tablets were stored in sealed HDPE-containers at 40°C/75% RH for 6 months ( Fig. 3A ) or at 25°C/60 % RH for 12 months ( Fig. 3B ). It can be seen that the tablet stability of the microcapsules of the invention is much better than that of tablets formed of FloraGLO Lutein 10 % VG TabGrade microcapsules.
  • the stability of the lutein ester microcapsules in powder form was tested in two beverages, an orange juice and a sport beverage.
  • the orange juice was prepared from diluted orange juice concentrate with added ascorbic acid and sodium benzoate. Lutein ester microcapsules as a powder corresponding to a final concentration of 30 ppm lutein were dissolved in the concentrate. The solution was treated in a high pressure homogenizer at 100 bar and filled into bottles. The bottles were stored at room temperature and normal daylight for 1 month. The stability (ring formation) was evaluated visually every week.
  • the sport beverage was prepared from carboxymethyl cellulose, water and a powder mix comprising calcium phosphate, potassium phosphate, sodium citrate, sodium chloride, sodium benzoate, potassium benzoate, citric acid, ascorbic acid and sucrose.
  • Lutein ester powder corresponding to a final concentration of 5 ppm lutein were dissolved in water and added to the sport beverage followed by pasteurization in 60 seconds of the mixture. After cooling the bottles were filled and stored for 1 month at room temperature in normal daylight. The stability (ring formation) was evaluated visually every week.
  • the powders comprising microcapsules prepared according to examples 4 and 5 were tested in orange juice and sport beverage. After 1 month storage none of the samples showed ring formation in the beverages, i.e. the samples had sufficient stability in these applications.
  • the powders comprising microcapsules prepared according to examples 1-4 were tested in milk. After 3 weeks storage none of the samples showed ring formation in milk i.e. the samples had sufficient stability in this application.
  • the invention is not reduced to the previously given examples but can be varied in many fold ways.
  • the following carotenoids or its esters can also be used: zeaxanthin, beta-carotene, alpha-carotene, lycopene, astaxanthin, canthaxanthin, beta-cryptoxanthin, citranaxanthin and beta-apo-8'-carotenoids.

Claims (17)

  1. Microcapsule comprenant au moins une substance active choisie parmi la lutéine et les esters de lutéine incorporés dans une matrice comprenant de la gélatine de poisson à faible bloom ayant une force de 100 blooms ou moins, et éventuellement un ou plusieurs autres composants de la matrice, où la teneur de ladite au moins une substance active est calculée en lutéine libre est de 0,5 à 25% du poids total de la microcapsule, et ladite microcapsule ne comprenant aucun émulsifiant ajouté.
  2. Microcapsule selon la revendication 1, dans laquelle la teneur de ladite au moins une substance active calculée en lutéine libre est de 1 à 20% du poids total de la microcapsule.
  3. Microcapsule selon les revendications 1 et 2, dans laquelle la teneur de ladite au moins une substance active calculée en lutéine libre est de 3 à 15% du poids total de la microcapsule.
  4. Microcapsule selon l'une quelconque des revendications 1 à 3, dans laquelle la teneur de ladite au moins une substance active calculée en lutéine libre est de 4 à 13% du poids total de la microcapsule.
  5. Microcapsule selon l'une quelconque des revendications 1 à 4, dans laquelle la teneur de ladite au moins une substance active calculée en lutéine libre est de 5 à 10% du poids total de la microcapsule.
  6. Microcapsule selon l'une quelconque des revendications 1 à 5, comprenant en outre au moins un antioxydant et / ou un plastifiant.
  7. Microcapsule selon l'une quelconque des revendications 1 à 6, dans laquelle ladite gélatine de poisson à faible bloom est une gélatine de poisson ayant une force de 80 blooms ou moins, telle que de 50 blooms ou moins, de préférence de 30 blooms ou moins, plus préférablement de 20 blooms ou moins, encore plus préférablement de 10 blooms ou moins, le plus préférablement de zéro bloom.
  8. Microcapsule selon l'une quelconque des revendications 1 à 7, préparée à partir d'une émulsion de lutéine ou d'ester de lutéine fondu ou dissous dans une solution aqueuse de ladite gélatine de poisson à faible bloom en absence d'un émulsifiant, ladite lutéine ou le ou les concentrés d'ester de lutéine sont éventuellement fondus ou dissous dans une huile comestible.
  9. Microcapsule selon l'une quelconque des revendications 1 à 8, dans laquelle ladite gélatine de poisson à faible bloom est le seul agent avec des propriétés de dispersion présentes dans la microcapsule.
  10. Procédé de préparation d'une microcapsule selon l'une quelconque des revendications 1 à 9, ledit procédé comprenant les étapes de
    • la fusion ou la dissolution de la lutéine ou du ou des concentrés d'esters de lutéine,
    • la fourniture d'une solution aqueuse de ladite gélatine de poisson à faible bloom et éventuellement d'autres composants de matrice,
    • le mélange de ladite solution aqueuse et ledit ou les concentrés de lutéine ou d'ester de lutéine fondus ou dissous,
    • l'homogénéisation de la préparation résultante sans ajout d'émulsifiant,
    • la division fine et le séchage du mélange ainsi obtenu pour préparer un masse de particules contenant chacune de la lutéine ou des esters de lutéine enrobés dans ladite gélatine de poisson à faible bloom.
  11. Procédé selon la revendication 10, dans lequel le ou les concentrés d'ester de lutéine sont fondus ou dissous dans une huile comestible, choisi dans le groupe des huiles végétales, par ex. huile de tournesol, huile d'olive, huile de coton, huile de carthame, huile de triglycérides à chaîne moyenne (TCM), huile de palme ou huile de palme hydrogénée.
  12. Procédé selon les revendications 10 ou 11, dans lequel ladite solution aqueuse de gélatine de poisson à faible bloom est ajoutée audit ou aux concentrés de lutéine ou d'ester de lutéine fondus ou dissous avant l'homogénéisation, ou dans lequel ledit ou les concentrés de lutéine ou d'ester de lutéine fondus ou dissous sont ajoutés à ladite solution aqueuse de gélatine de poisson à faible bloom avant l'homogénéisation.
  13. Procédé selon l'une quelconque des revendications 10 à 12, comprenant une autre étape d'homogénéisation.
  14. Microcapsule selon la revendication 1, pouvant être obtenue par un procédé comprenant les étapes de
    • la fusion ou la dissolution de la lutéine ou du ou des concentrés d'esters de lutéine,
    • la fourniture d'une solution aqueuse de ladite gélatine de poisson à faible bloom et éventuellement d'autres composants de matrice,
    • le mélange de ladite solution aqueuse et ledit ou les concentrés de lutéine ou d'ester de lutéine fondus ou dissous,
    • l'homogénéisation de la préparation résultante sans ajout d'émulsifiant,
    • la division fine et le séchage du mélange ainsi obtenu pour préparer un masse de particules
    contenant chacune de la lutéine ou des esters de lutéine enrobés dans ladite gélatine de poisson à faible bloom.
  15. Produit comprenant des microcapsules selon l'une quelconque des revendications 1 à 9 et 14 ou des microcapsules produites selon l'une quelconque des revendications 10 à 13.
  16. Produit selon la revendication 15, qui est un comprimé, un aliment, un complément alimentaire, une boisson, une laiterie, un produit pharmaceutique ou vétérinaire, un aliment ou un complément alimentaire, un produit de soins personnels ou un produit ménager.
  17. Produit selon la revendication 15 ou 16, ledit produit étant choisi parmi un comprimé, un produit laitier ou une boisson et comprenant des microcapsules selon l'une quelconque des revendications 1 à 9 ou des microcapsules produites selon l'une quelconque des revendications 10 à 13, dans lesquelles ladite gélatine de poisson est la gélatine de poisson à faible bloom ayant de préférence une force de 30 blooms ou moins.
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MX2021007517A (es) * 2018-12-18 2021-07-15 Quaker Oats Co Sistemas para producir aditivos alimenticios a partir de elementos alimenticios y metodos relacionados.
CN109805238A (zh) * 2019-01-31 2019-05-28 安徽仙奇生物工程技术有限公司 一种功能型固体饮料及制备方法
CN111150085B (zh) * 2019-12-31 2022-05-13 西昌市正中食品有限公司 一种复合包埋壁材以及微胶囊苦荞营养物、制备工艺
CN112869155A (zh) * 2021-01-18 2021-06-01 晨光生物科技集团股份有限公司 一种叶黄素酯水分散制剂及其制备方法和应用
CN113317427A (zh) * 2021-05-31 2021-08-31 晨光生物科技集团股份有限公司 一种用于压片的叶黄素酯制剂及其制备方法
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MY184987A (en) 2021-04-30
CN107205456A (zh) 2017-09-26
WO2016124785A1 (fr) 2016-08-11
KR20170115555A (ko) 2017-10-17
EP3253233A1 (fr) 2017-12-13
US10440983B2 (en) 2019-10-15
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US20180027865A1 (en) 2018-02-01
CN107205456B (zh) 2021-07-16

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